Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F4/00—Polymerisation catalysts
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
  • C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
  • C08F210/18—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers with non-conjugated dienes, e.g. EPT rubbers

Definitions

• This invention relates to the problem of preparing random terpolymers of ethylene, propylene and a diene, such as ethylidenenorbornene (ENB), dicyclopentadiene (DCPD), or 1,4-hexadiene (HD).
• ENB ethylidenenorbornene
• DCPD dicyclopentadiene
• HD 1,4-hexadiene
• EPDM is prepared in a Ziegler-Natta polymerization process that uses a catalyst system which comprises a Group IV-Group VII transition metal compound, e.g., a vanadium compound, as one component of the catalyst and a Group I-III organometallic compound, e.g., an alkylaluminum halide, as the other component of the catalyst.
• a catalyst system which comprises a Group IV-Group VII transition metal compound, e.g., a vanadium compound, as one component of the catalyst and a Group I-III organometallic compound, e.g., an alkylaluminum halide, as the other component of the catalyst.
• Vanadium compounds used for this process include VOCl 3 , VCL 4 , V(2,4-pentanedionate) 3 , and simple derivatives of these compounds.
• vanadium oxyhalides such as VOCl 3
• VOCl 3 vanadium oxyhalides
• the imido group ( ⁇ N--R) meets these requirements, and several vanadium imido complexes are known in the chemical literature.
• the present invention in its broadest embodiments uses a vanadium imido complex of the following general formula
• X is a group capable of forming a single bond to vanadium and R is a suitable hydrocarbyl substituent.
• the atom in X which bonds to vanadium can be a Group VA atom, such as nitrogen or phosphorus, a Group VIA atom, such as oxygen or sulfur, or a Group VIIA atom, such as chlorine, bromine or fluorine.
• Representative groups or atoms that may be selected for use as X include the halogens, and such hydrocarbyl (R) containing groups as --OR, --NR 2 , --SR, and --PR 2 .
• the group R (either attached to the nitrogen atom or in the X groups mentioned above) is hydrocarbyl such as alkyl, aryl, or alkyl-substituted aryl.
• the vanadium imido complexes which are preferred for use herein are those which have chlorine as the halogen atom and have the following formula:
• This invention employs such vanadium imido complexes as the vanadium containing component in a novel process for the preparation of EPDM.
• the catalyst composition of the present invention is analogous to known catalysts containing a vanadium oxyhalide component, e.g., VOCl 3 , and a suitable Group I-III organometallic cocatalyst compound, such as a dialkylaluminum halide (e.g., diethylaluminum chloride, isobutylaluminum chloride, and the like), a trialkylaluminum (e.g., triethylaluminum), a dialkylzinc (e.g., diethylzinc), or a dialkylmagnesium (e.g., diethylmagnesium).
• a dialkylaluminum halide e.g., diethylaluminum chloride, isobutylaluminum chloride, and the like
• a trialkylaluminum e.g., triethylaluminum
• a dialkylzinc e.g., diethy
• the novelty is the use of the aforementioned vanadium imido complexes where R can, for example, be alkyl, aryl, or alkyl-substituted aryl, for example, C 1 -C 20 alkyl, C 6 -C 20 aryl, and C 1 -C 20 alkyl-substituted aryl.
• R can, for example, be alkyl, aryl, or alkyl-substituted aryl, for example, C 1 -C 20 alkyl, C 6 -C 20 aryl, and C 1 -C 20 alkyl-substituted aryl.
• the length of the alkyl chain, if present either as such or as an alkyl substituent on an aryl ring, is not deemed especially critical to the performance of the catalyst.
• the halogen moieties in the vanadium imido complex are preferably chloro but bromo substituents could be substituted.
• the relative molar ratio of metal in the organoaluminum component to vanadium in the complex can range from about 1:1 to about 200:1.
• the catalyst can be utilized in 15 polymerization of ethylene, propylene and diene monomers using conventionally employed conditions (e.g., pressures of from about 0.1 bar to about 100 bars, preferably 1-10 bars and temperatures of from about -20° C. to about 100° C., preferably from 0° C. to about 60° C.).
• the reactor was charged with 500 mL hexane, 2.0 mL ethylidenenorbornene (ENB), and the desired amount of alkylaluminum halide cocatalyst as described below. Temperature control was established at 25° C., and the pressure in the reactor was allowed to equilibrate with atmospheric. The reactor was then pressurized to 2.0 psig with hydrogen. Propylene was admitted to the reactor until the total pressure reached 25 psig, and the reactor was finally pressurized to 50 psig with an equimolar mixture of ethylene and propylene. A pre-measured amount of the catalysts was then added to the reactor under pressure to begin polymerization. During polymerization, the temperature was allowed to rise to 30° C., and control was re-established. The pressure in the reactor was maintained at 50 psig by supplying an equimolar mixture of ethylene and propylene on demand.
• EOB ethylidenenorbornene
• the reactor contents were removed through a dip tube and collected in a jar containing 50 mL hexane and 5 mL isopropanol to kill the catalyst.
• the resulting polymer cement was poured into 3 liters of rapidly stirred isopropanol to precipitate the polymer product.
• the EPDM was then collected by decantation or filtration, dried, weighed and analyzed by standard techniques (ASTM D3900).

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• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
• Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

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• 1991
  • 1991-06-13 US US07/714,399 patent/US5086023A/en not_active Expired - Lifetime
• 1992
  • 1992-06-03 EP EP19920201592 patent/EP0518415A3/de not_active Withdrawn
  • 1992-06-12 KR KR1019920010254A patent/KR100200943B1/ko not_active IP Right Cessation
  • 1992-06-12 JP JP17767792A patent/JP3280706B2/ja not_active Expired - Fee Related

Non-Patent Citations (2)

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